Drawing No. EH–FM–021 // Fluid Mechanics & Piping
Pump NPSH Calculator
Reviewed August 2026
Calculate NPSH available and margin for an open or pressurized suction source, including water vapour pressure from temperature.
What problem does this solve?
Calculate net positive suction head available (NPSHa) and compare it with the pump manufacturer's NPSHr.
Inputs
Results
Background
Engineering basis, assumptions, interpretation and practical limitations.
NPSHa = surface pressure head + static head − suction losses + velocity head − vapour pressure head, all expressed as metres or feet of the pumped liquid.
Vapour pressure rises rapidly with temperature. That subtracts from NPSHa and can make hot-water or condensate service vulnerable to cavitation.
NPSHa belongs to the system. NPSHr belongs to the pump and operating point. Good design provides margin rather than merely making NPSHa equal to NPSHr.
Frequently Asked Questions
Practical questions about NPSHa, NPSHr, suction head and cavitation margin.
NPSHa is calculated from the suction system. NPSHr is supplied by the pump manufacturer for a particular flow and speed.
Yes. Enter a negative value when the pump centreline is above the liquid surface, creating suction lift.
The equation shown uses total head at the pump suction. Be consistent with the manufacturer definition and the location where losses are evaluated.
No. NPSH margin is important, but cavitation and recirculation behaviour also depend on pump design and operating point.